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Dortmund Data Bank
Thermophysical Data for Process Design
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Query
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DDB#
Name
CAS-RN
Formula
8
1,2-Ethanediol
107-21-1
C
2
H
6
O
2
Overview
Details
161
Toluene
108-88-3
C
7
H
8
Overview
Details
174
Water
7732-18-5
H
2
O
Overview
Details
237
Propane
74-98-6
C
3
H
8
Overview
Details
1051
Methane
74-82-8
CH
4
Overview
Details
Search for mixtures containing this mixture as subsystem
Search data for binary subsystems
Mixture Data
Databank
Sets
Points
Temperature
Range
Pressure
Range
Vapor-Liquid Equilibria
VLE
34
314
213-378 K
689-67879 kPa
8
174
1051
16
161
237
1051
15
174
237
1051
3
Gas Solubilities
GLE
5
12
263-283 K
15000-30000 kPa
8
174
1051
5
Activity Coefficients at Infinite Dilution (Binary Solvents)
ACM
4
21
273-323 K
n.a.
8
161
174
4
Liquid-Liquid Equilibria (Miscibility Gaps)
LLE
4
13
298-394 K
13790 kPa (const.)
8
161
174
3
161
174
1051
1
(A)zeotropic Data
AZD
1
1
233 K (const.)
n.a.
161
237
1051
1
Mixture Viscosities
VIS
8
74
265-473 K
3447-138080 kPa
8
174
1051
3
161
174
1051
5
Mixture Surface Tensions
MSFT
10
116
233-300 K
479-13789 kPa
8
174
1051
10
Mixture P-v-T Data
MPVT
2
9
272-300 K
3447-13789 kPa
8
174
1051
2
Gas Hydrate Data
GHD
125
885
229-353 K
115-1,5E6 kPa
8
174
237
7
8
174
237
1051
7
8
174
1051
35
8
237
1051
1
161
174
1051
2
174
237
1051
73
Further Thermodynamic Properties
X
13
188
231-378 K
100-55261 kPa
8
161
174
237
1051
1
8
161
174
1051
1
8
174
237
1
8
174
237
1051
2
8
174
1051
7
174
237
1051
1
Total
206
1633
8
161
174
7
8
161
174
237
1051
1
8
161
174
1051
1
8
174
237
8
8
174
237
1051
9
8
174
1051
78
8
237
1051
1
161
174
1051
8
161
237
1051
16
174
237
1051
77
Dortmund Data Bank Version: February 2024
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